WO2014123466A1 - Base d'avoine liquide - Google Patents

Base d'avoine liquide Download PDF

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Publication number
WO2014123466A1
WO2014123466A1 PCT/SE2014/000010 SE2014000010W WO2014123466A1 WO 2014123466 A1 WO2014123466 A1 WO 2014123466A1 SE 2014000010 W SE2014000010 W SE 2014000010W WO 2014123466 A1 WO2014123466 A1 WO 2014123466A1
Authority
WO
WIPO (PCT)
Prior art keywords
protein
oat
amylase
oats
deamidase
Prior art date
Application number
PCT/SE2014/000010
Other languages
English (en)
Inventor
Angeliki Triantafyllou
Original Assignee
Oatly Ab
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority to DK14749131.0T priority Critical patent/DK2953482T3/en
Priority to JP2015555962A priority patent/JP6511400B2/ja
Priority to RU2015125371A priority patent/RU2616802C2/ru
Priority to US14/759,449 priority patent/US9743684B2/en
Priority to MYPI2015001950A priority patent/MY181577A/en
Priority to PL14749131T priority patent/PL2953482T3/pl
Priority to SG11201504862QA priority patent/SG11201504862QA/en
Priority to AU2014215729A priority patent/AU2014215729B2/en
Priority to KR1020157024022A priority patent/KR101773155B1/ko
Priority to RS20190356A priority patent/RS58501B1/sr
Application filed by Oatly Ab filed Critical Oatly Ab
Priority to EP14749131.0A priority patent/EP2953482B1/fr
Priority to NZ709990A priority patent/NZ709990A/en
Priority to ES14749131T priority patent/ES2719698T3/es
Priority to CA2899717A priority patent/CA2899717C/fr
Priority to CN202211657198.1A priority patent/CN116420790A/zh
Priority to CN201480006081.4A priority patent/CN105007757A/zh
Publication of WO2014123466A1 publication Critical patent/WO2014123466A1/fr
Priority to HK16100525.6A priority patent/HK1212562A1/zh
Priority to US15/656,259 priority patent/US20170318841A1/en
Priority to HRP20190518TT priority patent/HRP20190518T1/hr
Priority to US17/386,167 priority patent/US20220015399A1/en

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Classifications

    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/52—Adding ingredients
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L7/00—Cereal-derived products; Malt products; Preparation or treatment thereof
    • A23L7/10—Cereal-derived products
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
    • A23C11/00—Milk substitutes, e.g. coffee whitener compositions
    • A23C11/02—Milk substitutes, e.g. coffee whitener compositions containing at least one non-milk component as source of fats or proteins
    • A23C11/10—Milk substitutes, e.g. coffee whitener compositions containing at least one non-milk component as source of fats or proteins containing or not lactose but no other milk components as source of fats, carbohydrates or proteins
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/38—Other non-alcoholic beverages
    • A23L2/382—Other non-alcoholic beverages fermented
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/52—Adding ingredients
    • A23L2/68—Acidifying substances
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
    • A23L33/10—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
    • A23L33/17—Amino acids, peptides or proteins
    • A23L33/185—Vegetable proteins
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
    • A23L33/30—Dietetic or nutritional methods, e.g. for losing weight
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L7/00—Cereal-derived products; Malt products; Preparation or treatment thereof
    • A23L7/10—Cereal-derived products
    • A23L7/104—Fermentation of farinaceous cereal or cereal material; Addition of enzymes or microorganisms
    • A23L7/107—Addition or treatment with enzymes not combined with fermentation with microorganisms
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2250/00—Food ingredients
    • A23V2250/54—Proteins
    • A23V2250/548—Vegetable protein
    • A23V2250/5484—Oat protein

Definitions

  • a liquid oat base and a process for preparing it using protein-deamidase are described in detail below.
  • the present invention relates to a liquid oat base, in particular a liquid oat base for use as a milk substitute or a food additive, and to a method for its manufacture.
  • Oat drinks for use as cow milk substitutes (EP 731646 Bl; EP 1124441 Bl; US 6451369 Bl) and as a raw material for other non-dairy milk products (US 7160564 B2) are known in the art. They are preferred by many customers for various reasons, such as for their content of soluble ⁇ -glucan fiber beneficial to health, their lack of potentially allergenic proteins and of lactose, which cannot be digested by the majority of the global population.
  • the soluble protein content of oat milk is about 0.5 to about 1.0 % by weight.
  • the starting material such as oat flour or oat bran or the whole oats from which it is made or an aqueous suspending or mixture of it is heated to a temperature and for a time sufficient to substantially prevent the development of endogenous enzymatic activity, in particular lipase/ lipoxygenase activity, but also ⁇ -glucanase activity, during the respective process.
  • Known oat drinks may be termed "oat bases" since, in addition to be used as drinks, in particular milk drinks, they can be used as a base for food other products, such as oat yogurt or oat batter, or be used as a food additive.
  • oat milk typically 0.5 % by weight
  • fat in form of vegetable oil such as rapeseed oil
  • EP 976 829 Al discloses a protein deamidating enzyme and a process for its production.
  • EP 1 371 734 Al discloses a method of denaturating milk protein by a deamidating enzyme to improve its sensitivity to protease and its emulsifying, foaming and gelling characteristics.
  • EP 1 839 491 discloses a dairy product and a method of its production by contacting milk with a deamidating enzyme to suppress acidic and bitter taste.
  • WO 2008/138900 A2 discloses a method for producing an acidified milk drink by contacting raw or processed milk with a deamidating enzyme.
  • Another object of the invention is to provide said
  • a further object of the invention is to provide a process for producing the improved oat drink or base.
  • an oat base of the aforementioned kind having an improved content of soluble oat protein.
  • "Improved protein content” is a higher protein content than obtainable by methods known in the art from a given oat raw material with the proviso that the improved content is not due to the use of protease (peptidase/proteinase) .
  • the oat base of the invention is provided by degrading an oats material with one or more amylases and protein-deamidase .
  • the protein-deamidase is one capable of deamidating high-molecular oat protein, such as oat globulin.
  • the protein-deamidase does not comprise substantial protease
  • protein-deamidase of the invention is preferably free from protease activity.
  • protein- deamidases useful in the invention are disclosed in EP 976829 Bl.
  • a preferred amount of protein-deamidase is from 0.5 - 20 U/g oat protein .
  • deamidation is carried out in parallel amidolysis, that is, with starch degradation by amylase (s) .
  • "In parallel with amidolysis” is understood as simultaneous with the enzymatic degradation of starch by amylase (s) .
  • deamidation of oat protein may however be continued even after amidolysis has ceased or substantially ceased.
  • the process of the invention can be stopped at a desired viscosity, such as at a viscosity of from 100 cP to 200 cP or from 50 cP to 100 cP or from 25 cP to 50 cP or from 10 cP to 25 cP (sp2/60 rpm/25 ⁇ 2 °C) .
  • a desired viscosity such as at a viscosity of from 100 cP to 200 cP or from 50 cP to 100 cP or from 25 cP to 50 cP or from 10 cP to 25 cP (sp2/60 rpm/25 ⁇ 2 °C) .
  • the process of the invention is
  • temperature being > 80 °C, preferably greater than 90 °C, in particular greater than 100 °C, such as about 105 °C, at which temperature heating for about 10 seconds is sufficient to destroy any enzymatic activity.
  • the improved oat base of the invention differs from prior art oat bases (oat drinks) by its increased content of soluble oat protein.
  • soluble signifies “water soluble”.
  • the improvement in soluble protein content obtainable by the method of the invention is 10 per cent by weight and up to 20 per cent by weight or more.
  • the content of soluble protein in the oat base is not one increased by addition of soluble protein to the base or to the raw material from which it is made or during the process by which it is manufactured but by use of an appropriate oat raw material and an appropriate protein solubilization process. It is preferable to use a raw material with a high content of protein preserved in its natural state. "Preserved in its (a) natural state” signifies that the protein in the raw material has not been denaturated or has only been denaturated to a minor extent, such as by 10 % by weight or 20 % by weight.
  • Oats used for producing oat drinks is dry- or wet-heated prior to use as starting material for producing oat bases or drinks.
  • the purpose with the heat treatment is twofold. On the one hand, the purpose is to destroy beta-glucanase present and/or to prevent it from being formed during starch hydrolysis so as to preserve water-soluble beta-glucans in their native state.
  • Beta- glucans in their native state are high-molecular beta-glucans, such as of a molecular weight of 50,000 D or more. High molecular beta-glucans are considered to constitute a valuable health- promoting component of oat drinks. Inactivation of beta-glucanase by heat treatment is however only indicated if the oat drink to be manufactures is desired to contain substantial amounts of beta-glucans .
  • the purpose with the traditional heat treatment is to inactivate lipase and lipoxygenase. Inactivation of lipase and lipoxygenase is
  • the need of inactivating lipase and lipoxigenase can be avoided by removing the lipids of the raw material, such as by extraction with ethanol or
  • water-soluble protein in untreated oats is about 60 % to about 70 % weight of total protein, it is only about 30 % weight in microwave-treated oats ( Skanemollan, Sweden) and in steam-treated (102 °C for 50 min, then air-dried (110 °C - 120 °C min for 50 min) oats.
  • this kind of heat treatment in particular steaming, should be avoided or at least be kept as short as possible and/or carried out at a temperature as low as possible to keep oat protein denaturation low. If avoided, the lipids should be removed from the oats. If heating is the preferred method of preventing the product from turning rancid and from preventing substantial degradation of ⁇ -glucan, a compromise between heating temperature and/or length of heating, at the one hand, and completeness of inactivation of ⁇ -glucanase and lipase/lipoxygenase, at the other hand is attempted.
  • a preferred raw material for use in the invention is dehulled or hulless/naked, dry milled oat flour that has not been heat treated, in particular steamed.
  • dry milled oat flour that has not been heat treated or dry milled flour of any oats fraction can also be used.
  • Particularly preferred is the use of dry milled non-heat treated oats, non-heat treated oat bran, and non-steamed oats.
  • heating of oats in any form at a temperature of up to about 50 °C or even up to about 65 °C for a few hours, such as for one or two or even five hours, does not result in substantial denaturation.
  • heating such oats material for a corresponding time period at a temperature of 80 °C or more does result in a substantial reduction of soluble protein, in particular if the material is in a humid state.
  • Steaming of oats in any form results in substantial denaturation, such as denaturation of 30 % or more and even of 50 % of more. Consequently, steamed oats materials, such as, for instance, those disclosed in US 6165365 A and US 7494683 B2, are not preferred for use in the present invention .
  • the oat base of the invention is prepared by milling groats (dehulled oats) with water to obtain a mash containing from 8 % by weight to 13 % by weight dry substance, then adding amylase (s) and degrading the oat starch at a temperature of from 50 °C to 75 °C.
  • the amylase may be beta- and alpha amylase or a mixture thereof, the amylases being added as a mixture or their mixture in the mash being formed by their simultaneous or sequential addition.
  • amylases are added in amount (s) sufficient for
  • amylase (s) are added in an amount to provide amylase activity of from 140 to 250 Betamyl-3 units and from 0.5 to 4 Ceralpha units per g of starch, in particular of about 180 Betamyl-3 units and about 1 Ceralpha unit per g of starch.
  • liquid oat base prepared by the process of the invention and a liquid oat base comprising oat protein deamidated by protein deamidase. It is preferred for the oat base protein to comprise 10 % by weight or 20 % by weight or more of protein deamidated by protein deamidase .
  • liquid oat base of the invention as a food, a food additive or a starting material for production of a food, all intended for human consumption.
  • Oat kernels Dehulled, steam treated, wet ground or dry ground .
  • Oat bran (Frebaco Kvarn AB, Lidkoping, Sweden) : Prepared from steam treated Swedish oat grain by grinding in a rolling mill.
  • Composition (% by weight) : Protein 18, fat 7, carbohydrate 45, fiber 16 %, water 9.5.
  • Enzymes Protein-glutaminase "Amano 50", 50 U/g (Amano Inc., Japan) .
  • Commercial alpha-amylase and beta-amylase are available from various commercial sources.
  • Alpha-amylase activity One Ceralpha unit is defined as the amount of enzyme required to release one micromole of p- nitrophenol from BPNPG7 (non-reducing end blocked p-nitrophenyl maltoheptaoside ) in one minute under defined assay conditions: http: //secure. megazyme. com/files/BOOKLET/K-BETA3_1010_DATA.pdf
  • Beta-amylase activity One ⁇ - ⁇ 3 (p-nitrophenyl-B-D- maltotrioside) unit is defined as the amount of enzyme required to release one micromole of p-nitrophenol from PNPp-G3 in one minute under defined assay conditions:
  • Protein-glutaminase activity One activity unit (U) is defined as the quantity of enzyme producing one ⁇ of ammonia per min in the reaction with 10 mM aqueous benzylocarbonyl-L- glutaminylglycine (Cbz-Gln-Gly) .
  • Viscosity Measured with a Brookfield Visco DV-II+
  • Dehulled, steam treated oat kernels (675 kg) were wet ground in a colloidal mill at a temperature of 54 °C and directly fed into a stainless steel enzyme treatment tank over a period of about 20 min. Stirring was started at a mash volume of about 100 L. About 7.5 L of an aqueous solution of alpha-and beta-amylase (1 Ceralpha unit per 180 Betamyl-3 units per g of starch) was used. Enzyme activity may vary depending on the commercial source of the enzymes; in this experiment the total weight of amylases was 432 g. The enzyme solution was fed into the tank in parallel with the mash over a period of about 12 min at the end of which about 3000 L of the mash had been fed into the tank. The rest of the mash was fed into the tank over a period of about 8 min to bring the total contents of the tank to about 5600 L. The temperature of the mash was kept constant at 56 °C.
  • PG Protein-glutaminase dosing.
  • PG (687.5 g) was dissolved in 1.5 L water at room temperature.
  • the PG solution was added to the mash at a viscosity of 160.5 (sp2/60 rpm/25 ⁇ 2 °C) .
  • Stirring was continued for about 120 min at a temperature of about 56 °C to reach a mash viscosity of 35 (sp2/60 rpm/25+2 °C) and a pH of 6.6. Any enzyme activity was then destroyed by heating the product to 95 °C.
  • the mash was cooled to room temperature and decanted. Decantation can be omitted if a whole grain product is to be produced.
  • enriched oat drink has a viscosity (sp2/60 rpm/25 ⁇ 2 °C) of 17.5 cP and a pH of 6.8.
  • the formulated oat drink or oat milk is transferred to a storage tank from which it is dispensed for UHT treatment and packaging.
  • Example 2 As Example 2 but with non-heat treated dry milled and sieved oat kernels, fraction size ⁇ 0.5 mm mixed with water to a dry weight of 11 %.
  • Product analysis Deamidation of product: 8.9 % of total releaseable ammonia.
  • Deamidation of control (non-enzymatic deamidation) : 1.5 % of total releaseable ammonia (same process in absence of PG) .
  • Soluble protein 81 % of total protein (product of the invention) v. 62 % of total protein (control) .
  • EXAMPLE 5 Deamidation of oat drink at laboratory and pilot plant scale by protein-glutaminase The oat base or drink used in the example was prepared according to the method disclosed in European patent no.
  • This oat drink is a commercial product manufactured by Oatly AB, Landskrona, Sweden.
  • Table 1 important features of a number of products according to the invention are shown. Also shown are corresponding features of deamidation products obtained from dry-milled heat-treated oats. The products were obtained in absence of deamidase (0 U) and in presence of deamidase at two deamidase addition regimes (1 U; 2x0.5 U/g oat protein) . From Table 1 it is evident that the content of total protein is substantially increased in the presence of deamidase. It is also evident that, at otherwise identical conditions, a non-heat treated starting material yields a product with higher protein content than a corresponding heat-treated starting material.

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  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Nutrition Science (AREA)
  • Health & Medical Sciences (AREA)
  • Biotechnology (AREA)
  • Mycology (AREA)
  • Microbiology (AREA)
  • Proteomics, Peptides & Aminoacids (AREA)
  • Cereal-Derived Products (AREA)
  • Non-Alcoholic Beverages (AREA)
  • Coloring Foods And Improving Nutritive Qualities (AREA)
  • Medicines Containing Plant Substances (AREA)
  • Grain Derivatives (AREA)

Abstract

L'invention concerne un procédé de préparation d'une base d'avoine liquide ou d'une boisson d'un contenu protéique d'avoine soluble amélioré à partir d'une matière d'avoine, en particulier une matière d'avoine qui n'a pas été thermotraitée à l'état humide, comprenant la solubilisation d'une protéine d'avoine dans un solvant aqueux au moyen de la protéine désamidase. L'invention concerne également une base d'avoine liquide correspondante et son utilisation.
PCT/SE2014/000010 2013-02-05 2014-01-28 Base d'avoine liquide WO2014123466A1 (fr)

Priority Applications (20)

Application Number Priority Date Filing Date Title
EP14749131.0A EP2953482B1 (fr) 2013-02-05 2014-01-28 Base d'avoine liquide
JP2015555962A JP6511400B2 (ja) 2013-02-05 2014-01-28 液状のエンバクベース
US14/759,449 US9743684B2 (en) 2013-02-05 2014-01-28 Liquid oat base
MYPI2015001950A MY181577A (en) 2013-02-05 2014-01-28 Liquid oat base
PL14749131T PL2953482T3 (pl) 2013-02-05 2014-01-28 Ciekła baza owsiana
SG11201504862QA SG11201504862QA (en) 2013-02-05 2014-01-28 Liquid oat base
AU2014215729A AU2014215729B2 (en) 2013-02-05 2014-01-28 Liquid oat base
NZ709990A NZ709990A (en) 2013-02-05 2014-01-28 Liquid oat base
RS20190356A RS58501B1 (sr) 2013-02-05 2014-01-28 Tečna ovsena baza
DK14749131.0T DK2953482T3 (en) 2013-02-05 2014-01-28 LIQUID OCEAN BASE
RU2015125371A RU2616802C2 (ru) 2013-02-05 2014-01-28 Жидкая овсяная основа
KR1020157024022A KR101773155B1 (ko) 2013-02-05 2014-01-28 액상 귀리 기제
ES14749131T ES2719698T3 (es) 2013-02-05 2014-01-28 Base de avena líquida
CA2899717A CA2899717C (fr) 2013-02-05 2014-01-28 Base d'avoine liquide
CN202211657198.1A CN116420790A (zh) 2013-02-05 2014-01-28 液体燕麦基料
CN201480006081.4A CN105007757A (zh) 2013-02-05 2014-01-28 液体燕麦基料
HK16100525.6A HK1212562A1 (zh) 2013-02-05 2016-01-18 液體燕麥基料
US15/656,259 US20170318841A1 (en) 2013-02-05 2017-07-21 Liquid oat base
HRP20190518TT HRP20190518T1 (hr) 2013-02-05 2019-03-15 Tekuća zobena baza
US17/386,167 US20220015399A1 (en) 2013-02-05 2021-07-27 Liquid oat base

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
SE1300087 2013-02-05
SE1300087-2 2013-02-05

Related Child Applications (2)

Application Number Title Priority Date Filing Date
US14/759,449 A-371-Of-International US9743684B2 (en) 2013-02-05 2014-01-28 Liquid oat base
US15/656,259 Continuation US20170318841A1 (en) 2013-02-05 2017-07-21 Liquid oat base

Publications (1)

Publication Number Publication Date
WO2014123466A1 true WO2014123466A1 (fr) 2014-08-14

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Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/SE2014/000010 WO2014123466A1 (fr) 2013-02-05 2014-01-28 Base d'avoine liquide

Country Status (19)

Country Link
US (3) US9743684B2 (fr)
EP (1) EP2953482B1 (fr)
JP (2) JP6511400B2 (fr)
KR (1) KR101773155B1 (fr)
CN (2) CN105007757A (fr)
AU (1) AU2014215729B2 (fr)
CA (1) CA2899717C (fr)
DK (1) DK2953482T3 (fr)
ES (1) ES2719698T3 (fr)
HK (1) HK1212562A1 (fr)
HR (1) HRP20190518T1 (fr)
MY (1) MY181577A (fr)
NZ (1) NZ709990A (fr)
PL (1) PL2953482T3 (fr)
PT (1) PT2953482T (fr)
RS (1) RS58501B1 (fr)
RU (1) RU2616802C2 (fr)
SG (1) SG11201504862QA (fr)
WO (1) WO2014123466A1 (fr)

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017171601A1 (fr) 2016-04-01 2017-10-05 Oatly Ab Base d'avoine et produit fermenté comprenant la base d'avoine présentant une viscosité améliorée
JP2018520693A (ja) * 2015-07-30 2018-08-02 オートリー・エービーＯａｔｌｙ ＡＢ 植物性健康飲料
WO2018219869A1 (fr) * 2017-05-29 2018-12-06 Creal Food Ab Procédé de préparation de fractions d'avoine ou d'orge
WO2019122499A1 (fr) * 2017-12-22 2019-06-27 Valio Ltd Produit à base de plantes et procédé correspondant
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LV15707A (lv) * 2021-08-13 2023-02-20 Darius Sargautis Metode dzēriena pagatavošanas no auzu materiāla
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WO2024084055A1 (fr) * 2022-10-21 2024-04-25 Société des Produits Nestlé S.A. ALIMENT LIQUIDE COMPRENANT DU β-GLUCANE ; HYDROLYSAT ISSU D'UN MATÉRIAU À BASE D'AVOINE ; ET PROCÉDÉS ASSOCIÉS

Families Citing this family (43)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10980244B2 (en) 2008-11-04 2021-04-20 The Quaker Oats Company Whole grain composition comprising hydrolyzed starch
US9510614B2 (en) 2008-11-04 2016-12-06 The Quaker Oats Company Food products prepared with soluble whole grain oat flour
US9504272B2 (en) 2008-11-04 2016-11-29 The Quaker Oats Company Method of processing oats to achieve oats with an increased avenanthramide content
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US10689678B2 (en) 2008-11-04 2020-06-23 The Quaker Oats Company Method and composition comprising hydrolyzed starch
BR112013024263A2 (pt) 2011-03-21 2016-12-27 Pepsico Inc método para preparar bebidas de grãos inteiros com alto ácido rdt
BR112014002956A8 (pt) 2011-07-12 2022-09-06 Pepsico Inc Método de preparar uma bebida láctea contendo aveia
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US20170275662A1 (en) 2016-03-22 2017-09-28 The Quaker Oats Company Method and Apparatus for Controlled Hydrolysis
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US11051536B2 (en) * 2018-07-19 2021-07-06 The Quaker Oats Company Oat bran composition comprising beta glucan and method of making
EP3911177A4 (fr) * 2019-01-18 2022-09-28 Ripple Foods, PBC Analogues non laitiers et boissons contenant des protéines végétales désamidés et procédés de préparation de tels produits
AU2020226258A1 (en) * 2019-02-21 2021-09-30 Amano Enzyme Europe Ltd. Prevention of aggregation in plant milk
EP3941215A4 (fr) * 2019-03-21 2023-01-18 Plant Tap, LLC Produit alimentaire à boire
CN111772108A (zh) * 2019-04-03 2020-10-16 内蒙古伊利实业集团股份有限公司 一种天然黑豆浸膏及其制备方法
CN115867144A (zh) * 2020-06-08 2023-03-28 天野酶制品株式会社 蛋白质口感改良
US12035723B1 (en) 2020-07-22 2024-07-16 Chobani Llc Oat flour based food composition and method of manufacture
US20230240312A1 (en) * 2020-08-24 2023-08-03 Amano Enzyme Inc. Plant milk treated with protein deamidase
CN114259001B (zh) * 2020-09-14 2023-07-28 统一企业(中国)投资有限公司昆山研究开发中心 复合酶制剂以及使用该复合酶制剂制得的饮料
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EP4005398A3 (fr) 2020-11-06 2022-10-05 Polar Glucan Oy Applications de farine d'avoine entière colloïdale instantanée
US11771121B1 (en) 2021-01-05 2023-10-03 Chobani Llc Plant-based zero sugar food product and associated method
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WO2023126061A1 (fr) * 2021-12-30 2023-07-06 Oatly Ab Composition d'avoine liquide et son procédé de production
CN114868852A (zh) * 2022-03-08 2022-08-09 武汉新华扬生物股份有限公司 一种用于液体燕麦基料的复配酶制剂及其使用方法
JPWO2023190734A1 (fr) * 2022-03-31 2023-10-05
CN115363100B (zh) * 2022-09-15 2023-08-04 草根知本集团有限公司 一种富含β-葡聚糖的植物蛋白饮料及其制备方法
BE1031148B1 (fr) 2022-12-16 2024-07-15 Meurens Natural Procédé de production d'un hydrolysat
CN115669852A (zh) * 2022-12-27 2023-02-03 河北科技大学 一种冲调型水溶性燕麦粉的制备方法
WO2024181555A1 (fr) * 2023-03-02 2024-09-06 天野エンザイム株式会社 Préparation enzymatique pour la production d'une composition liquide à base de plantes contenant du bêta-glucane

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6036983A (en) * 1996-05-20 2000-03-14 Novo Nordisk A/S Method of obtaining protein hydrolysates
WO2000030457A1 (fr) * 1998-11-20 2000-06-02 Kellogg Company Preparation enzymatique d'une base cereale
US20120034341A1 (en) * 2009-08-10 2012-02-09 A.G.V. Products Corp. Oligo-Saccharide Enhanced Oat-Based Drink for Treating Hyperlipidaemia and Hyperglycemia and Improving Gastrointestinal Function and Process for Preparing the Same by Tri-Enzyme Hydrolysis and Micro-Particle Milling

Family Cites Families (36)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3857967A (en) 1971-05-10 1974-12-31 Kikkoman Shoyu Co Ltd Preparation of food and beverages with peptidoglutaminase
CA1318171C (fr) 1988-06-29 1993-05-25 Victor T. Huang Produits a base de fecule pour cuisson ou chauffage au four a micro-ondes
US5082672A (en) 1989-06-21 1992-01-21 The United States Of American As Represented By The Secretary Of Agriculture Enzymatic deamidation of food proteins for improved food use
US4996063A (en) 1989-06-30 1991-02-26 The United States Of America, As Represented By The Secretary Of Agriculture Method for making a soluble dietary fiber composition from oats
CN1099839A (zh) * 1993-08-31 1995-03-08 韩国布鲁克斯维奇公司 门锁装置
SE502941C2 (sv) * 1993-09-15 1996-02-26 Lennart Lindahl Homogen och stabil cerealiesuspension och förfarande för dess framställning
GB9407104D0 (en) 1994-04-11 1994-06-01 Dalgety Plc Process for the preparation of food ingredients
DE69736247T2 (de) 1996-05-20 2007-05-24 Novozymes A/S Verfahren zur herstellung von proteinhydrolysate
JP2000513231A (ja) 1996-07-01 2000-10-10 ノボ ノルディスク アクティーゼルスカブ ベーキングにおけるデアミダーゼの利用
FR2771600B1 (fr) * 1997-11-28 2000-06-09 Gervais Danone Co Preparation de produits alimentaires par fermentation d'un melange de jus de soja et d'hydrolysat cerealier par streptococcus thermophilus
JP3609648B2 (ja) 1998-06-04 2005-01-12 天野エンザイム株式会社 新規蛋白質脱アミド酵素、それをコードする遺伝子、その製造法並びにその用途
US6251651B1 (en) 1998-06-04 2001-06-26 Amano Pharmaceutical Co., Ltd. Protein-deamidating enzyme, gene encoding the same, production process therefor, and use thereof
US6190708B1 (en) * 1998-10-19 2001-02-20 Cereal Base Ceba Ab Enzyme preparations for modifying cereal suspensions
US6451369B1 (en) * 1998-10-19 2002-09-17 Cereal Base Ceba Ab Non-dairy, ready-to-use milk substitute, and products made therewith
EP1124441B1 (fr) 1998-10-26 2007-09-05 Oatly AB Procede d'isolation d'une composition de beta-glucane a partir de l'avoine et produits fabriques a partir de celle-ci
JP2000354498A (ja) * 1999-06-14 2000-12-26 Ajinomoto Co Inc トランスグルタミナーゼ処理による穀粉原料からの糖類の製造方法
DE60021160T2 (de) 1999-12-03 2006-05-11 Amano Enzyme Inc., Nagoya Protein-deamiderendes Enzym, dafür kodierendes Gen, enzym-produzierendes Mikroorganismus, Verfahren zur Herstellung und Verwendung davon
SE0004107D0 (sv) 2000-11-10 2000-11-10 Ceba Ab Fermented product based on an oat suspension
JP3961956B2 (ja) 2001-02-27 2007-08-22 天野エンザイム株式会社 乳蛋白質の脱アミド化方法及び乳蛋白質の変性方法
SE0200735D0 (sv) * 2002-03-13 2002-03-13 Raisio Group Plc Food and feed composition and process
JP2005192457A (ja) * 2004-01-06 2005-07-21 Minoru Hishinuma 加工米食品及びその製造法
KR100554482B1 (ko) 2004-08-25 2006-03-03 씨제이 주식회사 귀리겨를 초미세 분말화하는 방법 및 상기 방법에 의하여얻어지는 귀리겨 초미세 분말로부터 추출된 귀리 성분을포함하는 음료 조성물
MY148140A (en) 2005-01-13 2013-02-28 Amano Enzyme Inc A processed meat product or a fish paste product and method for producing the same
EP1839491B1 (fr) 2005-01-13 2016-11-16 Ajinomoto Co., Inc. Produit laitier et procede pour le produire
JP2006238758A (ja) * 2005-03-02 2006-09-14 Minoru Hishinuma 穀類加工食品及びその製造法
EP1914298B1 (fr) 2005-07-07 2017-12-06 Amano Enzyme Inc. Procédé de production de bière ou de boisson de type bière
RU2342854C2 (ru) * 2006-12-25 2009-01-10 Веллеоутс Лимитед Биоовсяный пищевой продукт (варианты)
BRPI0811492B8 (pt) 2007-05-11 2018-05-08 Chr Hansen As método para produzir uma bebida láctea acidificada, bebida láctea acidificada, e, polipeptídeo isolado com atividade desamidase
JP4964710B2 (ja) * 2007-08-29 2012-07-04 群栄化学工業株式会社 β−グルカン含有穀物糖化物の製造方法
ES2389238T3 (es) 2008-06-19 2012-10-24 Ajinomoto Co., Inc. Alimento procesado y procedimiento de producción del mismo
ES2658645T3 (es) * 2009-01-16 2018-03-12 Dupont Nutrition Biosciences Aps Generación enzimática de lípidos funcionales a partir de extracto de fibra de cereal
JP5737647B2 (ja) * 2010-06-30 2015-06-17 Ｎｌｔテクノロジー株式会社 光学シートの貼り合せ方法
US20130157307A1 (en) * 2010-08-02 2013-06-20 Novozymes North America, Inc. Process of Producing A Fermentation Product
CO6480105A1 (es) * 2011-01-04 2012-07-16 Promotora De Innovacion En Biotecnologia S A S Promitec Santander S A S Proceso con adicion dosificada de materia prima y enzima para la produccion de malto dextrinas y jarabes de glucosa altamente concentrados a partir de almidones.
US8828462B2 (en) 2011-05-12 2014-09-09 Griffith Laboratories International, Inc. Method for preparing a proteinaceous vegetable flavor enhancer
DK2953482T3 (en) * 2013-02-05 2019-04-23 Oatly Ab LIQUID OCEAN BASE

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6036983A (en) * 1996-05-20 2000-03-14 Novo Nordisk A/S Method of obtaining protein hydrolysates
WO2000030457A1 (fr) * 1998-11-20 2000-06-02 Kellogg Company Preparation enzymatique d'une base cereale
US20120034341A1 (en) * 2009-08-10 2012-02-09 A.G.V. Products Corp. Oligo-Saccharide Enhanced Oat-Based Drink for Treating Hyperlipidaemia and Hyperglycemia and Improving Gastrointestinal Function and Process for Preparing the Same by Tri-Enzyme Hydrolysis and Micro-Particle Milling

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP2953482A4 *

Cited By (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018520693A (ja) * 2015-07-30 2018-08-02 オートリー・エービーＯａｔｌｙ ＡＢ 植物性健康飲料
EP3328212A4 (fr) * 2015-07-30 2019-02-13 Oatly AB Boisson santé végétale
KR102512028B1 (ko) 2016-04-01 2023-03-20 오틀리 아베 증가된 점도의 귀리 베이스 및 발효된 귀리 베이스 제품
KR20190003540A (ko) * 2016-04-01 2019-01-09 오틀리 아베 증가된 점도의 귀리 베이스 및 발효된 귀리 베이스 제품
WO2017171601A1 (fr) 2016-04-01 2017-10-05 Oatly Ab Base d'avoine et produit fermenté comprenant la base d'avoine présentant une viscosité améliorée
WO2018219869A1 (fr) * 2017-05-29 2018-12-06 Creal Food Ab Procédé de préparation de fractions d'avoine ou d'orge
WO2019122499A1 (fr) * 2017-12-22 2019-06-27 Valio Ltd Produit à base de plantes et procédé correspondant
CN111491522A (zh) * 2017-12-22 2020-08-04 维利奥有限公司 植物基产品和方法
WO2020109541A1 (fr) * 2018-11-29 2020-06-04 Creal Food Ab Procédé de préparation de fractions de céréales
WO2021260067A2 (fr) 2020-06-24 2021-12-30 Société des Produits Nestlé S.A. Procédé de traitement de compositions contenant des protéines
WO2021259940A2 (fr) 2020-06-24 2021-12-30 Société des Produits Nestlé S.A. Procédé de préparation d'un liquide contenant des protéines végétales
WO2022063833A1 (fr) 2020-09-25 2022-03-31 Société des Produits Nestlé S.A. Procédé de préparation d'un produit à base de plante fermenté contenant une protéine
LV15707A (lv) * 2021-08-13 2023-02-20 Darius Sargautis Metode dzēriena pagatavošanas no auzu materiāla
WO2023156562A1 (fr) 2022-02-18 2023-08-24 Meura S.A. Procédé de production de produits de substitution aux produits laitiers
BE1030280A1 (fr) 2022-02-18 2023-09-11 Meura S A Procédé et utilisation d’un équipement de traitement de matières premières d’origine végétale destinées à la fabrication de produits alimentaires
EP4242303A1 (fr) 2022-03-08 2023-09-13 Novozymes A/S Polypeptides de fusion avec inhibiteur de désamidase et domaines de désamidase
WO2023170177A1 (fr) 2022-03-08 2023-09-14 Novozymes A/S Polypeptides de fusion à domaines désamidase et inhibiteurs de désamidase
DE102023109092A1 (de) 2022-04-20 2023-10-26 Steinecker GmbH Herstellung von milchersatzprodukten
CN115413712A (zh) * 2022-09-15 2022-12-02 草根知本集团有限公司 一种燕麦奶及其制备方法
CN115413712B (zh) * 2022-09-15 2023-08-04 草根知本集团有限公司 一种燕麦奶及其制备方法
WO2024084055A1 (fr) * 2022-10-21 2024-04-25 Société des Produits Nestlé S.A. ALIMENT LIQUIDE COMPRENANT DU β-GLUCANE ; HYDROLYSAT ISSU D'UN MATÉRIAU À BASE D'AVOINE ; ET PROCÉDÉS ASSOCIÉS

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RS58501B1 (sr) 2019-04-30
PT2953482T (pt) 2019-05-13
MY181577A (en) 2020-12-29
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DK2953482T3 (en) 2019-04-23
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US9743684B2 (en) 2017-08-29
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CN105007757A (zh) 2015-10-28
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CA2899717A1 (fr) 2014-08-14
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KR20150113200A (ko) 2015-10-07
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ES2719698T3 (es) 2019-07-12
RU2015125371A (ru) 2017-03-13
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EP2953482A1 (fr) 2015-12-16

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